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flowrate at a wellhead vacuum of approximately 75 inches of water column would likely produce an <br /> effective ROI in excess of 80 feet An effective ROI of 80 feet will provide for the ability to extract <br /> residual TPHg beyond boring SB-17 <br /> Based on an effective ROI of 80 feet at a flowrate of 100 scfm, using VW-I as the vapor extraction <br /> well should provide sufficient vacuum influence for the entire on-site vadose zone and capillary <br /> fringe zone impacted soil plumes Designing the VES based on a flowrate of 100 scfm, rather than a <br /> lesser flowrate, is recommended to provide sufficient remedial coverage of the entire impacted soil <br /> ' areas <br /> ' Vapor samples collected during the VET were analyzed for TPHg and BTEX in order to evaluate the <br /> expected mass removal rate for a soil VES Calculations indicate that at an extraction rate of 100 <br /> scfm, approximately 1,000 pounds per day(ppd) of TPHg could be extracted from well VW-I at the <br /> time of VES start-up Based on the expected start-up TPHg vapor concentrations in excess of <br /> 125,000 mg/m3, a thermal oxidizer (therm-ox) will provide for the most economic treatment and <br /> ' atmospheric discharge of extracted soil gas At VES start-up, the maximum daily extraction rate will <br /> be limited by the maximum TPHg concentration that the selected therm-ox can process Typical <br /> ' maximum process concentrations range from approximately 7,500 ppm to 10,000 ppm (33,400 <br /> mg/m3 to 44,600 mg/m3)and are manufacturer specific <br /> Because the expected TPHg concentration in soil gas at the time of VES start-up will exceed the <br /> maximum process capacity of a therm-ox, extracted soil gas will initially require atmospheric <br /> ' dilution to reduce the influent concentration to approximately 7,500 ppm to 10,000 ppm Therefore, <br /> the total system process capacity for a 100 scfm VES (assuming therm-ox inlet TPHg concentrations <br /> of 33,000 mg/m3) is expected to be approximately 300 ppd <br /> 1 <br /> ProjectNo 58100-06-18A -12- December 9, 1996 <br />